Eawag, Swiss Federal Institute of Aquatic Science and Technology, CH-8600, Dübendorf, Switzerland.
Eawag, Swiss Federal Institute of Aquatic Science and Technology, CH-8600, Dübendorf, Switzerland; Silesian University of Technology, Faculty of Power and Environmental Engineering, Environmental Biotechnology Department, PL-44100, Gliwice, Poland.
Water Res. 2017 Oct 1;122:234-245. doi: 10.1016/j.watres.2017.05.018. Epub 2017 May 11.
The efficiency of ozone-based processes under various conditions was studied for the treatment of a surface water (Lake Zürich water, Switzerland) spiked with 19 micropollutants (pharmaceuticals, pesticides, industrial chemical, X-ray contrast medium, sweetener) each at 1 μg L. Two pilot-scale ozonation reactors (4-5 m h), a 4-chamber reactor and a tubular reactor, were investigated by either conventional ozonation and/or the advanced oxidation process (AOP) O/HO. The effects of selected operational parameters, such as ozone dose (0.5-3 mg L) and HO dose (O:HO = 1:3-3:1 (mass ratio)), and selected water quality parameters, such as pH (6.5-8.5) and initial bromide concentration (15-200 μg L), on micropollutant abatement and bromate formation were investigated. Under the studied conditions, compounds with high second-order rate constants k>10 M s for their reaction with ozone were well abated (>90%) even for the lowest ozone dose of 0.5 mg L. Conversely, the abatement efficiency of sucralose, which only reacts with hydroxyl radicals (OH), varied between 19 and 90%. Generally, the abatement efficiency increased with higher ozone doses and higher pH and lower bromide concentrations. HO addition accelerated the ozone conversion to OH, which enables a faster abatement of ozone-resistant micropollutants. Interestingly, the abatement of micropollutants decreased with higher bromide concentrations during conventional ozonation due to competitive ozone-consuming reactions, except for lamotrigine, due to the suspected reaction of HOBr/OBr with the primary amine moieties. In addition to the abatement of micropollutants, the evolution of the two main transformation products (TPs) of hydrochlorothiazide (HCTZ) and tramadol (TRA), chlorothiazide (CTZ) and tramadol N-oxide (TRA-NOX), respectively, was assessed by chemical analysis and kinetic modeling. Both selected TPs were quickly formed initially to reach a maximum concentration followed by a decrease of their concentrations for longer contact times. For the studied conditions, the TP's concentrations at the outlet of the reactors ranged from 0 to 61% of the initial parent compound concentration, CTZ being a more persistent TP against further oxidation than TRA-NOX. Finally, it was demonstrated in both reactors that the formation of bromate (BrO), a potentially carcinogenic oxidation by-product, could be controlled by HO addition with a general improvement on micropollutant abatement. Post-treatment by granular activated carbon (GAC) filtration enabled the reduction of micropollutants and TPs concentrations but no changes in bromate were observed. The combined algae assay showed that water quality was significantly improved after oxidation and GAC post-treatment, driven by the abatement of the spiked pesticides (diuron and atrazine).
研究了在不同条件下基于臭氧的工艺对 19 种微污染物(药物、农药、工业化学品、X 射线造影剂、甜味剂)进行处理的效率,每种污染物的浓度均为 1μg/L。通过常规臭氧氧化和/或高级氧化工艺(AOP)O/HO,研究了两个中试规模的臭氧氧化反应器(4-5m h),一个是四室反应器,另一个是管式反应器。考察了选定的操作参数(臭氧剂量(0.5-3mg/L)和 HO 剂量(O:HO=1:3-3:1(质量比)))和选定的水质参数(pH 值(6.5-8.5)和初始溴化物浓度(15-200μg/L))对微污染物去除和溴酸盐形成的影响。在所研究的条件下,与臭氧反应的二级速率常数 k>10M s 的化合物(>90%)即使在最低臭氧剂量为 0.5mg/L 时也能很好地去除。相反,仅与羟基自由基(OH)反应的三氯蔗糖的去除效率在 19%至 90%之间变化。通常,臭氧剂量越高、pH 值越高、溴化物浓度越低,去除效率就越高。HO 加加速了臭氧向 OH 的转化,这使得臭氧抗性微污染物的去除速度更快。有趣的是,在常规臭氧氧化过程中,由于竞争臭氧消耗反应,除拉莫三嗪外,随着溴化物浓度的升高,微污染物的去除效率降低,因为 HOBr/OBr 与伯胺部分的可疑反应。除了微污染物的去除,还通过化学分析和动力学建模评估了两种主要转化产物(TP)的演变,即氢氯噻嗪(HCTZ)和曲马多(TRA)的氯噻嗪(CTZ)和曲马多 N-氧化物(TRA-NOX)。两种选定的 TP 最初很快形成,达到最大浓度,然后随着接触时间的延长,其浓度下降。在所研究的条件下,反应器出口处 TP 的浓度范围为初始母体化合物浓度的 0 至 61%,CTZ 是比 TRA-NOX 更持久的 TP。最后,在两个反应器中都证明了通过 HO 加可以控制溴酸盐(BrO)的形成,溴酸盐是一种潜在的致癌氧化副产物,对微污染物的去除有普遍的改善。颗粒活性炭(GAC)过滤后的后处理能够降低微污染物和 TP 的浓度,但溴酸盐没有变化。藻类综合检测表明,氧化和 GAC 后处理后水质得到显著改善,这是由于添加的农药(氯嘧啶和莠去津)的去除。